US2604455A - Preparation and reactivation of foraminate catalysts - Google Patents
Preparation and reactivation of foraminate catalysts Download PDFInfo
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- US2604455A US2604455A US106968A US10696849A US2604455A US 2604455 A US2604455 A US 2604455A US 106968 A US106968 A US 106968A US 10696849 A US10696849 A US 10696849A US 2604455 A US2604455 A US 2604455A
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J25/00—Catalysts of the Raney type
- B01J25/04—Regeneration or reactivation
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J25/00—Catalysts of the Raney type
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/06—Washing
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S502/00—Catalyst, solid sorbent, or support therefor: product or process of making
- Y10S502/514—Process applicable either to preparing or to regenerating or to rehabilitating catalyst or sorbent
Definitions
- foraminate catalyst as used in this specification is meant one comprising particles or pieces, for example granules prepared by crushing, of an alloy comprising the desired catalytically active metal or metals together with one or more cthermetals more soluble in acid or-alkali or other extracting liquid than the desired catalytically active metal or metals, said alloy comprising at least'one phase in which atoms of the desired catalytically active metal or metals and of the aforesaid more soluble metal or metals are on the same crystal lattice and said particles or pieces havin'ga robust core of alloy and an outer active layer having a skeletal structure resulting from the partial or complete re- I moval by the extracting liquid of the more soluble metal-"or metals from the aforesaid phase or phases in said outer layer.
- the particles or pieces may be prepared in various ways, for example by crushing the cool alloy, and may be of various sizes, but are preferably /8" to It has already been proposed to prepare foraminate copper, nickel, cobalt and iron catalysts fromtheir corresponding. alloys with aluminium by treating the alloys with an aqueous alkali.
- the sodium aluminate thus produced is in equilibrium with aluminium hydroxide and caustic soda:
- a process for the preparation of foram inate catalysts which comprises treating an alloy, as hereinafter defined; with a, stream of an aqueous solution of alkali at an uninterrupted space-velocity of greater than 10 to remove at least afpo'rtion of the aluminium from the surface layers of the alloy, and subsequently, without intrruption of- 'flo'w, replacing the aqueous alkali with a stream of washing liquid comprising water, the velocity of saidstream being such as to preclude the deposition of, alumina on-the activated catalyst.
- Alloys suitable'ior use in the process 'oiithis invention are copper-aluminium alloys containferred.
- the alkali used for aluminium extraction should have an uninterrupted space velocity greater than '10 and preferably between 20 and 30. In this way the deposition-of alumina during the activation is largely prevented.
- the strean'1' 'j if aqueouscaustic soda is replaced without anyfi'n terruption of flow, by a stream of liquid suitable for washing the catalyst since this wouldflead to alumina deposition.
- the space velocity of, the washing liquid may be decreased to a valuebelow 10, but should not be decreased to avalue which leads to the deposition of alumina on thecatalyst.
- washing liquid it is preferred however to maintain the space velocity of the washing liquid at a value greater than v10 until the residual caustic soda and sodium aluminateretained in the free space be: tween the granules have been substantiallyree moved, after which the space velocity of the washing liquid can be altered if desired.
- suitable washing liquids are those which remove residual caustic soda and sodium aluminate; from the activated catalyst, but do not have a deleterious, effect upon the catalyst activity,-for example by further reaction with the constituents of the alloy. It'is possible, to employ awide range of-aqueou's liquids, but it'ispreferred to use water itself as the washing liquid.
- fspace velocity is meantithe volume of extracting liquid passing per hour" per unit volume occupied by-the catalyst in granula'rform.
- Activationand washing may be carriedout in a separate ves'sel'and 'the'activat'ed catalyst subsequently introduced into the'reactor or the activation may be carried out in the reaction vessel; provided of course',"that this is alkaliresist'ana
- the catalysts of the present invention may be reactivatedwithin the reaction vessel by treatment with alkali. Ingeneral itis preferred to remove from abo'ut5% bout '30"% of the aluminium at each activation; 5 The-total V 3 aluminium removed should not exceed '70% of the initial aluminium content.
- the catalysts of the present invention are par- By the term hydrogenation as used in this reaction in whichthe specification is meant a V I 7' H reacting molecule undergoes an ncrease n hydrogen content but in which there is no fission of the bond between two atoms in the molecule.
- Hydrogenation may result in the addition of 'hyd'rogen'to a multiple bond, ,for example the conversion of ethylene to ethane, or 'to a system of; multiple bonds whereby their. number is. .decreased, for example the conversion ofbu'tadiene tiibutene-Z and the 'conversion of benzene to 'cyclohexane, or it may result in adecrease in the "multiplicity of the bond, for example the con- Version of acetylene to ethylene.
- Themultiple bond or bonds' may' join like orunlikeatoms, examples being the groups 0, C Oand CEN.
- the'term dehydrogenation is meant a' reactionwhich efiects the removal of hydrogen as such;
- the hydrogen may be removed from a substance *giVingfrise either to the formation of one or'more multiple bonds,for exammethe conversion 7 of propane 'to propene, ethyl 1 alcohol to acetaldehyde', ethylamine'to ac'etonitrile, or to anincrease in the"multiplicity of a" bond, for example ethylene to acetylene, or to an incre'ase inthe' number of multiple bonds, for example but'ene-Z to butadiene.
- the hydrogen which reacts may combine with both atoms formerly joined by the bond as in the examples givn'ab'ove, or it may add to only one of the atoms, as in'the conversion'of carbon dioxide to carbon monoxide and water;
- freductive amination is .meant the conversion of an aldehyde oraketone to an amine by reaction with hydrogen .in the presence of" ammonia or primary or secondary amines,.for example 'the conversion of'acetaldehyde to ethyl: amine according to theequation:
- Example 1 no litres ofs" to A" r n les Ora ann luminium al y i which the ratio .by. weight copper: aluminiumwas 55 :45 were activated by plished in 5 hours.
- Eqcwmple 2 A'secondsample of the alloy used in Example 1 wasextracted with 0.4% caustic soda at 80 C. and a space Velocity of 30. The removal of 20% by weight of the original aluminium was accomhe. prq u t a ter washin with water at a space velocity of,30 was entirely free from any visible coating of alumina.
- Example 3 A second portion of. the alloy usedin Example 3 was extracted under-similar conditionsito remove 20% of the original aluminium, e ept .that' a space velocity of 25 wasemployed. The. product, after washing with water at the same space veloc ity was entirely free from visiblealumina. A 7
- a process for the preparation of .foraminate catalysts which comprises lt'reating an aneyis lected from copper-aluminium alloys I containing 40 to 80% by weight offcop'per, nickellaluminiiim alloys containingBO to-62% by weight 6f.
- catalysts which comprises treating an alloy se- -lected from copper aluminium alloys containing water, the velocity of said stream being such asto preclude the deposition of alumina on the-activated catalyst.
- a process for the preparation of foraminate catalysts which comprises treating an alloy selected from copper-aluminium alloys containing 40 to 80% by weight of copper, nickel-aluminium alloys containing 30 to 62% by weight of nickel, cobalt-aluminium alloys containing, 15 to 55% by weight of cobalt, and iron-aluminium alloys containing 30 to 55% by weight of iron, with a stream of an aqueous solution of alkali at anuninterrupted space velocity of greater than to remove at least a portion of the aluminium from the surface layers of the alloy, and subsequently without interruption of flow, replacing the aqueous alkali with a stream of washing liquidcomprising water, the space velocity of said streambeing greater than 10, until substantially "all of the residual alkali has been removed from the catalyst.
- a process for the preparation of foraminate catalysts which comprises treating an alloy selected from copper-aluminium alloys containing 40 to 80% by weight of copper, nickel-aluminium alloys containing 30to 62% by weight of nickel,
- cobalt-aluminium alloys containing to 55% by weight of cobalt and iron-aluminium alloys conmove at least a portion of the aluminium from the f surface layers of the alloy, and subsequently with out interruption of flow, replacing the aqueous alkali with a stream of washingliquid comprising water, the velocity of said stream being such as to preclude the deposition of alumina on the activated catalyst.
- a process for the preparation of foraminate catalysts which comprises treating an alloy selected from copper-aluminium alloys containing 50 to 60% by weight of copper, nickel-aluminium alloys containing 30 to 50% by weight of nickel, cobalt-aluminium alloys containing 30 to 50% by weight of cobalt, and iron-aluminium alloys containing 30 to 55 by weight of iron with a stream of an aqueous solution'of alkali at an uninterrupted space velocity of from to 30, to remove at least a portion of the aluminium from the surface layers of the alloy, "and subsequently without interruption of flow, replacing the aqueous alkali with a stream of washing liquid comprising water, the space velocity of said stream being greater than 10, until substantially all of the residual alkali has been removed from the catalyst.
- a process for the preparation of foraminate catalysts which comprises treating an alloy selected from copper-aluminium alloys containing 40 to 80% by weight of copper, nickel-aluminium alloys containing to 62% by weight of nickel, cobalt-aluminium alloys containing 15 to 55% by weight of cobalt, and iron-aluminium alloys containing 30 to by weight of ironwitha stream of an aqueous solution of alkali at an uninterrupted space velocity of greater than 10 to remove at least a portion of the aluminium from the surface layers of the alloy, and without interruption of flow, subsequently replacing the aqueous alkali with a streamof water, the velocity of said stream being such as to preclude the deposition of alumina on the activated catalyst.
- a process for the preparation of foraminate catalysts which comprises treating an alloy selected from copper-aluminium alloys containing 50 to by weight of copper, nickel-aluminium alloys containing 30 to 50% by weight of nickel, cobalt-aluminium alloys containingSO to 50% by weight of cobalt, and iron-aluminum alloys containing 30 to 55 by weight of iron with a stream of an aqueous solution of alkali at'an uninterrupted space velocity of greater than 10 to remove at least a portion of the aluminium from the surface layers of the alloy, and subsequently without interruption of flow, replacing the aqueous alkaliwith a stream of water, the velocity of said stream being such as to preclude the deposition of alumina on the activated'catalyst.
- a process for th preparation of foraminate catalysts which comprises treating an alloy selected from copper-aluminium alloys containing 50 to 60% by weight of copper, nickel-aluminium alloys containing 30 to 50% by Weight of nickel, cobalt-aluminium alloys containing 30 to 50% by weight of cobalt, and iron-aluminium alloys containing 30 to 55% by'weightof iron with a stream of an aqueous solutionof' alkali at an uninterrupted space velocity offrom 20 to 30, to remove at least a portion of the aluminium from the surface layers of the alloy, and subsequently without interruption of flow, replacing th aque- Ous alkali with a stream of water, the space velocity of said stream being greater than 10, until substantially all of the residual alkali has been removed from the catalyst.
- a process for the preparation of foraminate catalysts which comprises treating an alloy selected from copper-aluminium alloys containing 40 to 80% by weight of copper, nickel-aluminium alloys containing 30 to 62% by weightof nickel, cobalt-aluminium alloys containing 15 to 55% by weight of cobalt, and iron-aluminium alloys containing 30 to 55% by weight of iron with a stream of an aqueous solution of 0.5 to 10% by weight sodium hydroxide at an uninterrupted space velocity of greater than 10 to remove at least a portion of the aluminium from the sur-.
- a process for the preparation of -forami nate catalysts which comprises treating an alloy selected from copper-aluminiumalloys containing'50 to -60% lay-weight of -copper, nickelaluminium alloyscontaining'30 to"50%-by weight of nickel; cobalt-aluminium alloys containing 30 to 50% -'by' weight of cobalt and iron-aluminium alloys containing 30 to55% by weight-of-iron with anjaqueous solution of 05 to" 10% by weight beingsuch as to preclude the deposition of-alumina onthe activated catalyst.
- a process for the-preparation of-forami- -nate catalysts which comprises treating, at a -temperatureof from atmospheric to 100 C.;'a-n alloy selected fromcopper -aluminium alloys containing 40 to 80% by weight of copper, nickelaluminium alloys containing 30m 62 by'weight of nickel,- cobalt aluminium alloys containing to-55% by weight of cobalt, and iron-aluminium alloys containing 30 to 55%- by weight of iron;
- 'A process for the preparation of foraminate catalysts which comprises 'treating, at a temperature of from atmospheric to 100 C.,'an-alloy selected from copperaluminium-alloys containing 50 to 60% by weight of copper, nickel-aluminium alloys-containing 30 to 50%-by Weight of nickel,
- the space velocity of said stream 55 hate catalysts which comprises treatingan alloy selected from copper-aluminium alloys containing 40 to 80% by weightpf copper, nickel-aluminalloys containings 30 to-62-% by weight of 10' to remove from- 5% to 30% by weight of the initial aluminium content, and subsequently,
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Description
i atenteci STATES PATENT PREPARATION AND Assaults, 6F" 7 FORAMI NATE CATALYSTS v I Peter William Reynolds and Ralph Lozelu Robinl s'on, Norton-on-Tees, England; assignors .:to;-; J p- Imperial Chemical. Industries Limited, a corporation of Great Britain 1 1 I v I No Drawing. Application Julyi 26, 1949; serial No. 106,968, 11; QreatBritainAugustB, 1948' 1': Claims. (01.252-412) This invention relates to the preparation of foraminate' catalysts."- I
By the" term "foraminate catalyst as used in this specification is meant one comprising particles or pieces, for example granules prepared by crushing, of an alloy comprising the desired catalytically active metal or metals together with one or more cthermetals more soluble in acid or-alkali or other extracting liquid than the desired catalytically active metal or metals, said alloy comprising at least'one phase in which atoms of the desired catalytically active metal or metals and of the aforesaid more soluble metal or metals are on the same crystal lattice and said particles or pieces havin'ga robust core of alloy and an outer active layer having a skeletal structure resulting from the partial or complete re- I moval by the extracting liquid of the more soluble metal-"or metals from the aforesaid phase or phases in said outer layer. The particles or pieces may be prepared in various ways, for example by crushing the cool alloy, and may be of various sizes, but are preferably /8" to It has already been proposed to prepare foraminate copper, nickel, cobalt and iron catalysts fromtheir corresponding. alloys with aluminium by treating the alloys with an aqueous alkali.
The aluminium in these alloys is readily attacked by aqueous caustic soda according to the equation:
The sodium aluminate thus produced is in equilibrium with aluminium hydroxide and caustic soda:
Thereis therefore a considerable danger that the activity of catalysts prepared by this method will be impaired by the presence of alumina on or near the surface of alumina will have the effect of decreasing the available active surface of the catalyst and so decreasing its activity. It will also'inmany cases promote undesirable side reactions and in extreme cases the alumina may be sufficient to cause an increased pressure drop through the catalyst bed and to cement together the catalyst granules making their discharge from the converter extremely difficult.
'According to the, present invention, there is provided a process for the preparation of foram inate catalysts which comprises treating an alloy, as hereinafter defined; with a, stream of an aqueous solution of alkali at an uninterrupted space-velocity of greater than 10 to remove at least afpo'rtion of the aluminium from the surface layers of the alloy, and subsequently, without intrruption of- 'flo'w, replacing the aqueous alkali with a stream of washing liquid comprising water, the velocity of saidstream being such as to preclude the deposition of, alumina on-the activated catalyst. ,i
. Alloys suitable'ior use in the process 'oiithis invention are copper-aluminium alloys containferred. Aqueous caustic soda solutions of from 0.5
to 10% strength by-weight areparticularly suit able. These maybe used at temperatures from atmospheric up to 1 00? C.or above. 7 It is essential for the process of the present invention that the alkali used for aluminium extraction should have an uninterrupted space velocity greater than '10 and preferably between 20 and 30. In this way the deposition-of alumina during the activation is largely prevented. After the extraction of the required quantity ofaluminium the strean'1' 'j:if aqueouscaustic soda is replaced without anyfi'n terruption of flow, by a stream of liquid suitable for washing the catalyst since this wouldflead to alumina deposition. The space velocity of, the washing liquid may be decreased to a valuebelow 10, but should not be decreased to avalue which leads to the deposition of alumina on thecatalyst. I
It is preferred however to maintain the space velocity of the washing liquid at a value greater than v10 until the residual caustic soda and sodium aluminateretained in the free space be: tween the granules have been substantiallyree moved, after which the space velocity of the washing liquid can be altered if desired. In gfen eral, suitable washing liquids are those which remove residual caustic soda and sodium aluminate; from the activated catalyst, but do not have a deleterious, effect upon the catalyst activity,-for example by further reaction with the constituents of the alloy. It'is possible, to employ awide range of-aqueou's liquids, but it'ispreferred to use water itself as the washing liquid. By the term fspace velocity is meantithe volume of extracting liquid passing per hour" per unit volume occupied by-the catalyst in granula'rform.
Activationand washing may be carriedout in a separate ves'sel'and 'the'activat'ed catalyst subsequently introduced into the'reactor or the activation may be carried out in the reaction vessel; provided of course',"that this is alkaliresist'ana Furthermore, the catalysts of the present invention may be reactivatedwithin the reaction vessel by treatment with alkali. Ingeneral itis preferred to remove from abo'ut5% bout '30"% of the aluminium at each activation; 5 The-total V 3 aluminium removed should not exceed '70% of the initial aluminium content.
The catalysts of the present invention are par- By the term hydrogenation as used in this reaction in whichthe specification is meant a V I 7' H reacting molecule undergoes an ncrease n hydrogen content but in which there is no fission of the bond between two atoms in the molecule.
Hydrogenation may result in the addition of 'hyd'rogen'to a multiple bond, ,for example the conversion of ethylene to ethane, or 'to a system of; multiple bonds whereby their. number is. .decreased, for example the conversion ofbu'tadiene tiibutene-Z and the 'conversion of benzene to 'cyclohexane, or it may result in adecrease in the "multiplicity of the bond, for example the con- Version of acetylene to ethylene. vThemultiple bond or bonds'may' join like orunlikeatoms, examples being the groups 0, C Oand CEN.
By the'term dehydrogenationis meant a' reactionwhich efiects the removal of hydrogen as such; The hydrogen may be removed from a substance *giVingfrise either to the formation of one or'more multiple bonds,for exammethe conversion 7 of propane 'to propene, ethyl 1 alcohol to acetaldehyde', ethylamine'to ac'etonitrile, or to anincrease in the"multiplicity of a" bond, for example ethylene to acetylene, or to an incre'ase inthe' number of multiple bonds, for example but'ene-Z to butadiene. When the formation of multiple bondsgives rise to an aromatic system as in'theconversion of cyclohexane to benzene, this t ype of dehydrogenation reaction may be termed aromatisation. In other forms of the "process; dehydrogenation is accompanied by thei'forrnation of aringgas in theconversion of hexane to benzene, orby the. formation; of open chain compounds containing more carbon atoms, asi'nthe conversionof ethylene to butadiene.
' [By the term hydrqgenolysis"" is meant areactlo'n'in; which hydrg'gen addition is ac'companied byjthefis'sion offone or, more bonds the'moleculeofthe'reacting substances." This maylead to fragmentation of the molecule, as in the conversiorr'of benzyl alcohol to toluene and water and the conversion of furfural t'o sylvan and wateryor it'may result in theopening of a ring as ln the conversion of cyclopropanel to propane.
The hydrogen which reacts may combine with both atoms formerly joined by the bond as in the examples givn'ab'ove, or it may add to only one of the atoms, as in'the conversion'of carbon dioxide to carbon monoxide and water; By'the term freductive amination, is .meant the conversion of an aldehyde oraketone to an amine by reaction with hydrogen .in the presence of" ammonia or primary or secondary amines,.for example 'the conversion of'acetaldehyde to ethyl: amine according to theequation:
Exam e am 4 Below u i a e.th ,.nrqesof the p e e i en ixamp es 1 ca 3 a e included for comparative purposes.
Example 1 no litres ofs" to A" r n les Ora ann luminium al y i which the ratio .by. weight copper: aluminiumwas 55 :45 were activated by plished in 5 hours.
treatment with 0.4% by weightaqu'eous caustic soda at C. at a spaceivelocit'y"of'4. After 28 hours 20% of the original aluminium had been l surface was blackened. 10
Eqcwmple 2 A'secondsample of the alloy used in Example 1 wasextracted with 0.4% caustic soda at 80 C. and a space Velocity of 30. The removal of 20% by weight of the original aluminium was accomhe. prq u t a ter washin with water at a space velocity of,30 was entirely free from any visible coating of alumina.
Example 3 Example 4 A second portion of. the alloy usedin Example 3 was extracted under-similar conditionsito remove 20% of the original aluminium, e ept .that' a space velocity of 25 wasemployed. The. product, after washing with water at the same space veloc ity was entirely free from visiblealumina. A 7
xample 5 Catalysts prepared asdescribed in Examples 1 and 2 were'used for the vapour phase conversion of iso-propanol to acetoneat a temperature of '35.0 C. The isopropanolwas fed'to the apparatus with av liquid space velocity of' 4. TheTfollowing results were obtained.
Per Ccnt yPer Cent Catalyst pass yield; pass yield Propylene acetone Catalyst prepared in Example 1 Catalyst prepared in Example 2;.
It is evident from these results that tiieusih the preparation of the'catalyst of a high space velocity of extracting alkali leads to the productron of a catalyst giving a. superior pass "yield fo f acetone and a very muchlower pass yield ofTundesired propylene.
l. A process for the preparation of .foraminate catalysts, which comprises lt'reating an aneyis lected from copper-aluminium alloys I containing 40 to 80% by weight offcop'per, nickellaluminiiim alloys containingBO to-62% by weight 6f. cobalt-aluminiumalloys containing 154th .55 ,"1' weight of cobalt, andiron aluminiumall"ys containing 30 to 55%1 by weightldfiroiifwfih or an aqueous soluti'oiiiof alliali at fa u rupted space velocity-ofgreatr than 10 at .least a portion orl the aluminiumfrom t facelayers of the alloy,..and subsequently with.-
catalysts which comprises treating an alloy se- -lected from copper aluminium alloys containing water, the velocity of said stream being such asto preclude the deposition of alumina on the-activated catalyst.
3. A process for the preparation of foraminate catalysts which comprises treating an alloy selected from copper-aluminium alloys containing 40 to 80% by weight of copper, nickel-aluminium alloys containing 30 to 62% by weight of nickel, cobalt-aluminium alloys containing, 15 to 55% by weight of cobalt, and iron-aluminium alloys containing 30 to 55% by weight of iron, with a stream of an aqueous solution of alkali at anuninterrupted space velocity of greater than to remove at least a portion of the aluminium from the surface layers of the alloy, and subsequently without interruption of flow, replacing the aqueous alkali with a stream of washing liquidcomprising water, the space velocity of said streambeing greater than 10, until substantially "all of the residual alkali has been removed from the catalyst.
4. A process for the preparation of foraminate catalysts which comprises treating an alloy selected from copper-aluminium alloys containing 40 to 80% by weight of copper, nickel-aluminium alloys containing 30to 62% by weight of nickel,
cobalt-aluminium alloys containing to 55% by weight of cobalt and iron-aluminium alloys conmove at least a portion of the aluminium from the f surface layers of the alloy, and subsequently with out interruption of flow, replacing the aqueous alkali with a stream of washingliquid comprising water, the velocity of said stream being such as to preclude the deposition of alumina on the activated catalyst.
. 5. A process for the preparation of foraminate catalysts which comprises treating an alloy selected from copper-aluminium alloys containing 50 to 60% by weight of copper, nickel-aluminium alloys containing 30 to 50% by weight of nickel, cobalt-aluminium alloys containing 30 to 50% by weight of cobalt, and iron-aluminium alloys containing 30 to 55 by weight of iron with a stream of an aqueous solution'of alkali at an uninterrupted space velocity of from to 30, to remove at least a portion of the aluminium from the surface layers of the alloy, "and subsequently without interruption of flow, replacing the aqueous alkali with a stream of washing liquid comprising water, the space velocity of said stream being greater than 10, until substantially all of the residual alkali has been removed from the catalyst. 6. A process for the preparation of foraminate catalysts which comprises treating an alloy selected from copper-aluminium alloys containing 40 to 80% by weight of copper, nickel-aluminium alloys containing to 62% by weight of nickel, cobalt-aluminium alloys containing 15 to 55% by weight of cobalt, and iron-aluminium alloys containing 30 to by weight of ironwitha stream of an aqueous solution of alkali at an uninterrupted space velocity of greater than 10 to remove at least a portion of the aluminium from the surface layers of the alloy, and without interruption of flow, subsequently replacing the aqueous alkali with a streamof water, the velocity of said stream being such as to preclude the deposition of alumina on the activated catalyst.
7. A process for the preparation of foraminate catalysts which comprises treating an alloy selected from copper-aluminium alloys containing 50 to by weight of copper, nickel-aluminium alloys containing 30 to 50% by weight of nickel, cobalt-aluminium alloys containingSO to 50% by weight of cobalt, and iron-aluminum alloys containing 30 to 55 by weight of iron with a stream of an aqueous solution of alkali at'an uninterrupted space velocity of greater than 10 to remove at least a portion of the aluminium from the surface layers of the alloy, and subsequently without interruption of flow, replacing the aqueous alkaliwith a stream of water, the velocity of said stream being such as to preclude the deposition of alumina on the activated'catalyst.
8. A process for th preparation of foraminate catalysts which comprises treating an alloy selected from copper-aluminium alloys containing 50 to 60% by weight of copper, nickel-aluminium alloys containing 30 to 50% by Weight of nickel, cobalt-aluminium alloys containing 30 to 50% by weight of cobalt, and iron-aluminium alloys containing 30 to 55% by'weightof iron with a stream of an aqueous solutionof' alkali at an uninterrupted space velocity offrom 20 to 30, to remove at least a portion of the aluminium from the surface layers of the alloy, and subsequently without interruption of flow, replacing th aque- Ous alkali with a stream of water, the space velocity of said stream being greater than 10, until substantially all of the residual alkali has been removed from the catalyst.
9. A process for the preparation of foraminate catalysts which comprises treating an alloy selected from copper-aluminium alloys containing 40 to 80% by weight of copper, nickel-aluminium alloys containing 30 to 62% by weightof nickel, cobalt-aluminium alloys containing 15 to 55% by weight of cobalt, and iron-aluminium alloys containing 30 to 55% by weight of iron with a stream of an aqueous solution of 0.5 to 10% by weight sodium hydroxide at an uninterrupted space velocity of greater than 10 to remove at least a portion of the aluminium from the sur-.
face layers of the alloy, and subsequently without interruption of flow, replacing the aqueous alkali to 50% by weight of cobalt and iron-aluminium alloys containing 30 to 55% by weight of iron with an aqueous solution of 0.5 to 10% by weight sodium hydroxide at an uninterrupted space velocity of greater than 10 to remove at least a por-v tion of the aluminium from the surface layers of the alloy, and subsequently without interruption of flow, replacing the aqueousalkali with a stream oizw ater, the-spacevelocit of said stream being greater than: until substantially all of the residual sodium hydroxide and sodium aluminate chaverbeen removed from the-catalyst.
11. A process for the preparation of -forami nate catalysts-which comprises treating an alloy selected from copper-aluminiumalloys containing'50 to -60% lay-weight of -copper, nickelaluminium alloyscontaining'30 to"50%-by weight of nickel; cobalt-aluminium alloys containing 30 to 50% -'by' weight of cobalt and iron-aluminium alloys containing 30 to55% by weight-of-iron with anjaqueous solution of 05 to" 10% by weight beingsuch as to preclude the deposition of-alumina onthe activated catalyst.
' 12.;A process for the-preparation of-forami- -nate catalysts which comprises treating, at a -temperatureof from atmospheric to 100 C.;'a-n alloy selected fromcopper -aluminium alloys containing 40 to 80% by weight of copper, nickelaluminium alloys containing 30m 62 by'weight of nickel,- cobalt aluminium alloys containing to-55% by weight of cobalt, and iron-aluminium alloys containing 30 to 55%- by weight of iron;
with a stream of an aqueous solution of alkali at :an uninterrupted space velocity of greater-than 10 to remove atleast a portion of the'aluminium from the surface layers-of the alloy,- and subsequently without-interruption of flow, replacing the aqueous alkali with a stream of washing liquid comprising water, the velocity of said stream being such as to preclud the deposition fof alumina on the activated catalyst.
13. 'A process for the preparation of foraminate catalysts which comprises 'treating, at a temperature of from atmospheric to 100 C.,'an-alloy selected from copperaluminium-alloys containing 50 to 60% by weight of copper, nickel-aluminium alloys-containing 30 to 50%-by Weight of nickel,
i cobalt-aluminium alloys-containing 30 to 50 by 1 weight of cobalt, and iron-aluminium alloys-containing 30 to 55% by weight of iron-with-a stream of-anaqueous solution of "alkali-at an uninterrupte d space velocity of greater than- 10 to-remove at least a portion of thealuminium from the surface layers of the alloy, and subsequently,
ous alkali with a stream of washing liquid comprising water, the space velocity of said stream 55 hate catalysts which comprises treatingan alloy selected from copper-aluminium alloys containing 40 to 80% by weightpf copper, nickel-aluminalloys containings 30 to-62-% by weight of 10' to remove from- 5% to 30% by weight of the initial aluminium content, and subsequently,
without interruption of flow, replacing the aqueous alkali with a stream of washing liquid com- .i'p'r'ising-waten the velocity of said stream being I such as to' preclude the deposition of aluminaon he'igactlva'it'ed'catalyst, i
2:8 I 15.A proces'sxfor the preparationofforaminatewfcatalysts which;comprises: treating'=an;-alloy selected from: fcopper-aluminium:-alloyscontaining 50rto' 60% by Weight o1 Tcopper; nickelalu- 5 Ii'linilimFGJHOyS'jCGHtalDlDgFBO -to 50% by -weight of onickel; cobalt aluminium alloys containing 30 -to--50%; by weight of cobalt, and iron-aluminium "alloyscontaining 30 to 55% "by weight of iron withvan aqueous solution containing 0.5 to 10% 10 -by :Weightofcso'dium hydroxide at an uninterruptedispacervlocity of from-{f to :30, "to remove from- 5 to':?30%--by;weight of the initial aluminium, content; andsubsequently without interrup- -tion of flow; replacing the aqueous-alkali with -a 15 stream 01" water; the space velocity of'saidstream being greater than 10, until substantially -a11= of a the residual sodium hydroxideand-sodium. alu- -minate= has been removed from-the catalyst.
lfiprocess for-the rreactivation of forami- 20 nate' catalysts which comprises-'- treating; the deac'tivated. "catalyst? originally? prepared from an :alloy' selected from.-copperealuminium alloyscon- "$ai'nl1'1g 40,tO '80 by we'ightof" copper, 1 nickelaluminiumalloys containing 30-to '62 by weight of! nickel, cobalt-aluminium alloys containing-l5 4:0 55% by w'eight of cobalt and iron-aluminium alloysicontaining to -55 :by weight ofoiron, withastream' of an aqueous solution of" alkali, at an un'interrupted "space-velocity 'ofzzgrater 30 than '10 to remove-a furtherl portionofr theraluminium without interruption of flow, subsequenti lyir'eplacing the-aqueousalkali with-ta stream' of "washing-1 liquid comprisingwaterjthe velocity? of said stream being such to preclude thedepo'sb *tion :ofpalu'mina onthevzactivate'd catalyst. 0.
"173A process" for the reactivation of forami- Y natei'catalysts' "which: comprises treating aideactivated catalyst originally prepared from i an 'allo'yselected'irom copper-aluminium alloys con- 40 warning: to Y 60 by' weight of' copper,- ni'ckelaluminium alloys contaimhgeo to 50 by Weight of nickeLfcobalt alurninium alloys containing- 30 to '50 of cobalt;andiron aluminium alloys containing 30 to by weight'bf iron, with a 1i stream: of arr-aqueous solution of 015" 'to *'''10%by weight of sodium hydroxide, at anuninter'rupted space velocity offrom 20' to -30 to remove a furthen-portion "of from 5 to "30% by weight ofthe initial aluminium content of the alloy,"without interruption of flow, subsequently replacing the aqueous alkali with a stream of water; the-space velocity of 'said stream being-greater than10, 'until substantially all of the residualsodiunfhyd-ro'iide' and sodiumaluminate has" been removed from the catalyst.
RALPH LOZELUTtOBlNSGN.
REFERENCESI CITED Thefollowing references are of record in the ,iile of this pate-nt: I r
UNITED STATES "PATENTS "Number 7 7 "Name Date 2 257300 Howk Oct. 7,1941 '2';391 ,283 Weber "Dec.' 18,1945
7- Qlishiedl-May-25r1943.
Claims (1)
1. A PROCESS FOR THE PREPARATION OF FORAMINATE CATALYSTS WHICH COMPRISES TREATING AN ALLOY SELECTED FROM COPPER-ALUMINIUM ALLOYS CONTAINING 40 TO 80% BY WEIGHT OF COPPER, NICKEL-ALUMINIUM ALLOYS CONTAINING 30 TO 62% BY WEIGHT OF NICKEL, COBALT-ALUMINIUM ALLOYS CONTAINING 15 TO 55% BY WEIGHT OF COBALT, AND IRON-ALUMINIUM ALLOYS CONTAINING 30 TO 55% BY WEIGHT OF IRON, WITH A STREAM OF AN AQUEOUS SOLUTION OF ALKALI AT AN UNINTERRUPTED SPACE VELOCITY OF GREATER THAN 10 TO REMOVE AT LEAST A PORTION OF THE ALUMINIUM FROM THE SURFACE LAYERS OF THE ALLOY, AND SUBSEQUENTLY WITHOUT INTERRUPTION OF FLOW, REPLACING THE AQUEOUS ALKALI WITH A STREAM OF WASHING LIQUID COMPRISING WATER, THE VELOCITY OF SAID STREAM BEING SUCH AS TO PRECLUDE THE DEPOSITION OF ALUMINA ON THE ACTIVATED CATALYST.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB21391/48A GB642861A (en) | 1948-08-13 | 1948-08-13 | Improvements in and relating to the preparation of foraminate catalysts |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2604455A true US2604455A (en) | 1952-07-22 |
Family
ID=10162131
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US106968A Expired - Lifetime US2604455A (en) | 1948-08-13 | 1949-07-26 | Preparation and reactivation of foraminate catalysts |
Country Status (4)
| Country | Link |
|---|---|
| US (1) | US2604455A (en) |
| DE (1) | DE846249C (en) |
| FR (1) | FR992765A (en) |
| GB (1) | GB642861A (en) |
Cited By (19)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2840619A (en) * | 1956-07-25 | 1958-06-24 | Exxon Research Engineering Co | Hydrogenation catalyst and use in oxo process |
| US2863928A (en) * | 1958-12-09 | Esters over cu-zn-ai catalysts | ||
| US2908722A (en) * | 1956-09-07 | 1959-10-13 | Air Reduction | Process for preparing saturated monohydric alcohols |
| US2950260A (en) * | 1957-12-09 | 1960-08-23 | Du Pont | Process of activating nickel-aluminum catalysts |
| US3096160A (en) * | 1961-06-19 | 1963-07-02 | Union Carbide Corp | Vapor diffusion coating process |
| US3139408A (en) * | 1961-12-21 | 1964-06-30 | Huseyin V Tumer | Process for preparing raney nickel catalyst |
| US3157735A (en) * | 1961-06-27 | 1964-11-17 | Aluminum Co Of America | Metallic particle compositions for mechanically joined electrical conductors |
| US3412042A (en) * | 1962-04-28 | 1968-11-19 | Kyowa Hakko Kogyo Kk | Hydrogenation catalyst composition consisting of aluminum, copper and cadmium |
| US3471575A (en) * | 1962-04-28 | 1969-10-07 | Shiro Kudo | Catalytic hydrogenation of alpha,beta-unsaturated carbonyl compounds,unsaturated fatty acids,and unsaturated fatty acid esters |
| US3691093A (en) * | 1969-02-12 | 1972-09-12 | Du Pont | Efficiency of nickel-aluminum catalysts by water washing |
| FR2211287A1 (en) * | 1972-12-25 | 1974-07-19 | Toyo Soda Mfg Co Ltd | |
| US3980720A (en) * | 1972-12-25 | 1976-09-14 | Toyo Soda Manufacturing Co., Ltd. | Method of producing diol by hydrogenolysis of peroxide polymers with reactivation of Raney nickel catalyst |
| US4014820A (en) * | 1974-04-05 | 1977-03-29 | Nalco Chemical Company | Method of making a Raney copper catalyst and the catalyst so made |
| US4090872A (en) * | 1976-12-29 | 1978-05-23 | The United States Of America As Represented By The Secretary Of The Air Force | Aluminum base brazing alloy |
| US4188498A (en) * | 1977-05-18 | 1980-02-12 | Nissan Chemical Industries, Ltd. | Process for producing linalool |
| US4292208A (en) * | 1974-05-03 | 1981-09-29 | Alloy Surfaces Company, Inc. | Diffusion coating combinations |
| US4349612A (en) * | 1978-11-24 | 1982-09-14 | Alloy Surfaces Company, Inc. | Metal web |
| US4375003A (en) * | 1978-07-13 | 1983-02-22 | Nalco Chemical Company | Method for the hydrogenation of nitriles to primary amines |
| FR2773086A1 (en) * | 1997-12-29 | 1999-07-02 | Rhone Poulenc Fibres | PROCESS FOR REGENERATION OF A HYDROGENATION CATALYST PROCESS FOR HYDROGENATION OF COMPOUNDS INCLUDING NITRILE FUNCTIONS |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA1006180A (en) * | 1973-10-19 | 1977-03-01 | Nalco Chemical Company | Method of producing acrylamide with a raney copper catalyst |
| EP1140356A1 (en) * | 1998-12-01 | 2001-10-10 | Novartis AG | Process for preparation of aminocarboxylic acids |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2257800A (en) * | 1940-04-12 | 1941-10-07 | Du Pont | Alloy-skeleton catalyst |
| US2391283A (en) * | 1942-04-11 | 1945-12-18 | Du Pont | Process for the hydrogenation of benzene |
| GB611987A (en) * | 1946-05-29 | 1948-11-05 | Peter William Reynolds | Improvements in and relating to catalysts |
| GB621749A (en) * | 1946-05-03 | 1949-04-19 | Peter William Reynolds | Improvements in and relating to catalysts and their use |
-
1948
- 1948-08-13 GB GB21391/48A patent/GB642861A/en not_active Expired
-
1949
- 1949-07-26 US US106968A patent/US2604455A/en not_active Expired - Lifetime
- 1949-07-30 DE DEP3680A patent/DE846249C/en not_active Expired
- 1949-08-12 FR FR992765D patent/FR992765A/en not_active Expired
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2257800A (en) * | 1940-04-12 | 1941-10-07 | Du Pont | Alloy-skeleton catalyst |
| US2391283A (en) * | 1942-04-11 | 1945-12-18 | Du Pont | Process for the hydrogenation of benzene |
| GB621749A (en) * | 1946-05-03 | 1949-04-19 | Peter William Reynolds | Improvements in and relating to catalysts and their use |
| GB611987A (en) * | 1946-05-29 | 1948-11-05 | Peter William Reynolds | Improvements in and relating to catalysts |
Cited By (23)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2863928A (en) * | 1958-12-09 | Esters over cu-zn-ai catalysts | ||
| US2840619A (en) * | 1956-07-25 | 1958-06-24 | Exxon Research Engineering Co | Hydrogenation catalyst and use in oxo process |
| US2908722A (en) * | 1956-09-07 | 1959-10-13 | Air Reduction | Process for preparing saturated monohydric alcohols |
| US2950260A (en) * | 1957-12-09 | 1960-08-23 | Du Pont | Process of activating nickel-aluminum catalysts |
| US3096160A (en) * | 1961-06-19 | 1963-07-02 | Union Carbide Corp | Vapor diffusion coating process |
| US3157735A (en) * | 1961-06-27 | 1964-11-17 | Aluminum Co Of America | Metallic particle compositions for mechanically joined electrical conductors |
| US3139408A (en) * | 1961-12-21 | 1964-06-30 | Huseyin V Tumer | Process for preparing raney nickel catalyst |
| US3412042A (en) * | 1962-04-28 | 1968-11-19 | Kyowa Hakko Kogyo Kk | Hydrogenation catalyst composition consisting of aluminum, copper and cadmium |
| US3471575A (en) * | 1962-04-28 | 1969-10-07 | Shiro Kudo | Catalytic hydrogenation of alpha,beta-unsaturated carbonyl compounds,unsaturated fatty acids,and unsaturated fatty acid esters |
| US3691093A (en) * | 1969-02-12 | 1972-09-12 | Du Pont | Efficiency of nickel-aluminum catalysts by water washing |
| FR2211287A1 (en) * | 1972-12-25 | 1974-07-19 | Toyo Soda Mfg Co Ltd | |
| US3896051A (en) * | 1972-12-25 | 1975-07-22 | Toyo Soda Mfg Co Ltd | Method of reactivation of raney nickel |
| US3980720A (en) * | 1972-12-25 | 1976-09-14 | Toyo Soda Manufacturing Co., Ltd. | Method of producing diol by hydrogenolysis of peroxide polymers with reactivation of Raney nickel catalyst |
| US4014820A (en) * | 1974-04-05 | 1977-03-29 | Nalco Chemical Company | Method of making a Raney copper catalyst and the catalyst so made |
| US4292208A (en) * | 1974-05-03 | 1981-09-29 | Alloy Surfaces Company, Inc. | Diffusion coating combinations |
| US4090872A (en) * | 1976-12-29 | 1978-05-23 | The United States Of America As Represented By The Secretary Of The Air Force | Aluminum base brazing alloy |
| US4188498A (en) * | 1977-05-18 | 1980-02-12 | Nissan Chemical Industries, Ltd. | Process for producing linalool |
| US4375003A (en) * | 1978-07-13 | 1983-02-22 | Nalco Chemical Company | Method for the hydrogenation of nitriles to primary amines |
| US4349612A (en) * | 1978-11-24 | 1982-09-14 | Alloy Surfaces Company, Inc. | Metal web |
| FR2773086A1 (en) * | 1997-12-29 | 1999-07-02 | Rhone Poulenc Fibres | PROCESS FOR REGENERATION OF A HYDROGENATION CATALYST PROCESS FOR HYDROGENATION OF COMPOUNDS INCLUDING NITRILE FUNCTIONS |
| WO1999033561A1 (en) * | 1997-12-29 | 1999-07-08 | Rhodia Fiber And Resin Intermediates | Method for regenerating a hydrogenation catalyst, method for hydrogenating compounds comprising nitrile functions |
| US6518449B1 (en) * | 1997-12-29 | 2003-02-11 | Rhodia Fiber & Resin Intermediates | Method for regenerating a hydrogenation catalyst, method for hydrogenating compounds comprising nitrile functions |
| KR100529200B1 (en) * | 1997-12-29 | 2005-11-17 | 로디아 폴리아미드 인터미디에이츠 | Method for regenerating a hydrogenation catalyst, method for hydrogenating compounds comprising nitrile functions |
Also Published As
| Publication number | Publication date |
|---|---|
| DE846249C (en) | 1952-08-11 |
| FR992765A (en) | 1951-10-23 |
| GB642861A (en) | 1950-09-13 |
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